CN113106514A - Electroplating heat energy recycling system and method - Google Patents
Electroplating heat energy recycling system and method Download PDFInfo
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- CN113106514A CN113106514A CN202110282032.5A CN202110282032A CN113106514A CN 113106514 A CN113106514 A CN 113106514A CN 202110282032 A CN202110282032 A CN 202110282032A CN 113106514 A CN113106514 A CN 113106514A
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- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25D—PROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
- C25D7/00—Electroplating characterised by the article coated
- C25D7/06—Wires; Strips; Foils
- C25D7/0607—Wires
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- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25D—PROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
- C25D21/00—Processes for servicing or operating cells for electrolytic coating
- C25D21/02—Heating or cooling
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- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25D—PROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
- C25D5/00—Electroplating characterised by the process; Pretreatment or after-treatment of workpieces
- C25D5/34—Pretreatment of metallic surfaces to be electroplated
- C25D5/36—Pretreatment of metallic surfaces to be electroplated of iron or steel
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- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25D—PROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
- C25D5/00—Electroplating characterised by the process; Pretreatment or after-treatment of workpieces
- C25D5/48—After-treatment of electroplated surfaces
- C25D5/50—After-treatment of electroplated surfaces by heat-treatment
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F27—FURNACES; KILNS; OVENS; RETORTS
- F27D—DETAILS OR ACCESSORIES OF FURNACES, KILNS, OVENS, OR RETORTS, IN SO FAR AS THEY ARE OF KINDS OCCURRING IN MORE THAN ONE KIND OF FURNACE
- F27D17/00—Arrangements for using waste heat; Arrangements for using, or disposing of, waste gases
- F27D17/004—Systems for reclaiming waste heat
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P10/00—Technologies related to metal processing
- Y02P10/25—Process efficiency
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- Electrochemistry (AREA)
- Materials Engineering (AREA)
- Metallurgy (AREA)
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- Environmental & Geological Engineering (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Coating With Molten Metal (AREA)
Abstract
The invention discloses an electroplating heat energy recycling system and method, wherein the system comprises a first circulating system and a second circulating system which are sequentially arranged; the first circulating system comprises a naked furnace outlet water cooling tank and a plurality of acid tanks which are sequentially arranged, a first heat exchanger is arranged in each acid tank, and hot water in the naked furnace outlet water cooling tank and cold water in the first heat exchanger circulate; the second circulating system comprises a hot water washing tank and an intermediate frequency furnace outlet water cooling tank which are sequentially arranged, and hot water in the intermediate frequency furnace outlet water cooling tank and cold water in the hot water washing tank circulate. The invention utilizes the cooling water of the steel wires at the outlets of the open-fire furnace and the intermediate frequency furnace to heat the liquid in the electroplating tank body which needs to be heated, thereby reducing the steam consumption and the production cost.
Description
Technical Field
The invention belongs to the technical field of electroplating, and particularly relates to an electroplating heat energy recycling system and method.
Background
In the production of the steel cord, the surface of the steel wire needs to be electroplated, the steel wire needs to be subjected to open-furnace heat treatment and intermediate-frequency furnace heat diffusion treatment in the electroplating process, and in addition, the liquid in a plurality of tanks needs to be heated to a certain temperature when the liquid is used for treating the steel wire in the electroplating process. After the steel wire is subjected to heat treatment by an electroplating open-fire furnace and heat diffusion treatment by an intermediate frequency furnace, the steel wire needs to be subjected to water cooling treatment, and cooling water needs to be subjected to cooling treatment by using cooling circulating water; when the electroplating line is produced, the acid tank, the plating tank, the hot water washing tank and the soap dipping tank need to use a large amount of steam to heat liquid in the tank body, so that the temperature of the liquid in the tank body is kept, and the production cost is very high.
Disclosure of Invention
The invention aims to overcome the defects in the prior art and provide an electroplating heat energy recycling system and method.
The invention provides the following technical scheme:
an electroplating heat energy recycling system comprises a first circulating system and a second circulating system which are arranged in sequence;
the first circulating system comprises a naked furnace outlet water cooling tank and a plurality of acid tanks which are sequentially arranged, a first heat exchanger is arranged in each acid tank, and hot water in the naked furnace outlet water cooling tank and cold water in the first heat exchanger circulate;
the second circulating system comprises a hot water washing tank and an intermediate frequency furnace outlet water cooling tank which are sequentially arranged, and hot water in the intermediate frequency furnace outlet water cooling tank and cold water in the hot water washing tank circulate.
Furthermore, the outlet water cooling tank of the open fire furnace is connected with the inlet end of the first heat exchanger through a filtering circulating pump, and the outlet end of the first heat exchanger is connected with the outlet water cooling tank of the open fire furnace.
Furthermore, the number of the acid tanks is three, the acid tanks comprise a first acid tank, a second acid tank and a third acid tank which are sequentially arranged, two first heat exchangers are arranged in each acid tank, and the first heat exchangers are PP heat exchangers.
Furthermore, the intermediate frequency furnace outlet cooling tank is connected with the inlet end of a water cooling tank pipeline pump, the outlet end of the water cooling tank pipeline pump is connected with the hot water washing tank, the hot water washing tank is connected with the inlet end of the hot water washing tank pipeline pump, and the outlet end of the hot water washing tank pipeline pump is connected with the intermediate frequency furnace outlet cooling tank.
Furthermore, the second circulating system further comprises a coating bath arranged at the front end of the hot water washing bath and a first small cooling bath arranged at the rear end of the outlet water cooling bath of the intermediate frequency furnace, the coating bath is connected with a second heat exchanger, the inlet end of the second heat exchanger is connected with the outlet end of the water cooling bath pipeline pump, and the outlet end of the second heat exchanger is connected with the first small cooling bath.
Further, a third heat exchanger is connected between the outlet end of the second heat exchanger and the first small cooling tank, the second heat exchanger is a plating tank plate heat exchanger, and the third heat exchanger is a cooling plate heat exchanger.
Further, the second circulating system further comprises a soap soaking groove arranged at the rear end of the water cooling groove at the outlet of the intermediate frequency furnace, a fourth heat exchanger is arranged in the soap soaking groove, the inlet end of the fourth heat exchanger is connected with the outlet end of the water cooling groove pipeline pump, the outlet end of the fourth heat exchanger is connected with the first small cooling groove, and the fourth heat exchanger is a stainless steel heat exchanger.
Furthermore, a second small cooling tank and a phosphating tank are sequentially arranged between the first small cooling tank and the soap soaking tank.
The electroplating heat energy recycling method adopts the electroplating heat energy recycling system and comprises the following steps:
cooling the steel wire treated by the open fire furnace in a water cooling tank at the outlet of the open fire furnace, heating the cooling water to be hot water at the temperature of 90 +/-5 ℃, filtering the hot water, then feeding the hot water into a first heat exchanger of an acid tank, heating acid liquid in the acid tank to the temperature of 65 +/-5 ℃, and returning cold water generated after heat exchange to the water cooling tank at the outlet of the open fire furnace;
the steel wire after the intermediate frequency furnace is handled cools down in intermediate frequency furnace export water cooling tank, heats the cooling water for 90 +/-5 ℃ hot water, and the hot water flows into hot water wash bowl, makes the temperature in the hot water wash bowl heat to 86 +/-5 ℃, and the steel wire makes the water cooling in the hot water wash bowl after the surface is washd in hot water wash bowl to flow back to intermediate frequency furnace export water cooling tank.
Furthermore, hot water in the water cooling tank at the outlet of the intermediate frequency furnace is also divided into a second heat exchanger connected with the plating tank and a fourth heat exchanger in the soap dipping tank for heating, plating solution in the plating tank enters the second heat exchanger to be heated to 49 +/-5 ℃, the temperature of lubricant in the soap dipping tank is heated to 77 +/-5 ℃ through the fourth heat exchanger, and cold water generated by the second heat exchanger and the fourth heat exchanger flows into a first small cooling tank at the rear end of the water cooling tank at the outlet of the intermediate frequency furnace.
Compared with the prior art, the invention has the beneficial effects that:
(1) according to the invention, the hot water generated by the water cooling tank at the outlet of the open fire furnace is used for heating the acid liquid in each acid tank, and the cold water generated after heat exchange flows back to the outlet of the open fire furnace for cooling, so that heat circulation is realized, additional steam or cooling equipment is not required, and the production cost is reduced;
(2) according to the invention, hot water generated by the cooling tank at the outlet of the intermediate frequency furnace is used for heating the plating solution in the plating tank, the cleaning water in the hot water washing tank and the lubricant in the soap dipping tank, and cold water generated after heat exchange flows back to be used for cooling steel wires, so that heat circulation is realized, additional steam or cooling equipment is not required, and the production cost is reduced;
(3) the electroplating heat energy recycling system provided by the invention has the advantages that the needed equipment is simple, the electroplating heat energy recycling system can be obtained only by modifying the original electroplating line, the operation cost is low, and the electroplating heat energy recycling system is suitable for popularization.
Drawings
FIG. 1 is a schematic structural diagram of an electroplating heat energy recycling system;
FIG. 2 is a schematic structural view of a first circulation system;
FIG. 3 is a schematic structural view of a second circulation system;
labeled as: 1. a water cooling tank at the outlet of the open fire furnace; 2. a filtration circulating pump; 3. a first acid tank; 4. a second acid tank; 5. a third acid tank; 6. a first heat exchanger; 7. plating bath; 8. a hot water washing tank; 9. an intermediate frequency furnace; 10. an outlet water cooling tank of the intermediate frequency furnace; 11. a first small cooling tank; 12. a second small cooling tank; 13. a phosphating tank; 14. a soap dipping tank; 15. a second heat exchanger; 16. a hot water tank washing pipeline pump; 17. a third heat exchanger; 18. a water cooling tank pipeline pump; 19. a fourth heat exchanger; 20. a steel wire.
Detailed Description
The invention is further described below with reference to the accompanying drawings. The following examples are only for illustrating the technical solutions of the present invention more clearly, and the protection scope of the present invention is not limited thereby.
It should be noted that in the description of the present invention, the terms "front", "rear", "left", "right", "upper", "lower", "inner", "outer", and the like indicate orientations or positional relationships based on the orientations or positional relationships shown in the drawings, and are only for convenience of describing the present invention but do not require that the present invention must be constructed and operated in a specific orientation, and thus, should not be construed as limiting the present invention.
As shown in fig. 1 to 3, the present embodiment provides an electroplating heat recycling system, which includes a first circulation system and a second circulation system sequentially disposed.
As shown in fig. 1 and 2, the first circulation system comprises a water cooling tank 1 at the outlet of the open fire furnace and a plurality of acid tanks which are arranged in sequence, wherein a first heat exchanger 6 is arranged in each acid tank, and hot water in the water cooling tank 1 at the outlet of the open fire furnace and cold water in the first heat exchanger 6 circulate. The outlet water cooling tank 1 of the open fire furnace is connected with the inlet end of a first heat exchanger 6 through a filtering circulating pump 2, and the outlet end of the first heat exchanger 6 is connected with the outlet water cooling tank 1 of the open fire furnace. The number of the acid tanks is three, the acid tanks comprise a first acid tank 3, a second acid tank 4 and a third acid tank 5 which are arranged in sequence, two first heat exchangers 6 are arranged in each acid tank, and the first heat exchangers 6 are PP heat exchangers.
As shown in fig. 1 and 3, the second circulation system includes a hot water washing tank 8, an intermediate frequency furnace 9, and an intermediate frequency furnace outlet water cooling tank 10, which are sequentially arranged, and hot water in the intermediate frequency furnace outlet water cooling tank 10 circulates with cold water in the hot water washing tank 8. The intermediate frequency furnace outlet cooling tank 10 is connected with the inlet end of a water cooling tank pipeline pump 18, the outlet end of the water cooling tank pipeline pump 18 is connected with the hot water washing tank 8, the hot water washing tank 8 is connected with the inlet end of a hot water washing tank pipeline pump 16, and the outlet end of the hot water washing tank pipeline pump 16 is connected with the intermediate frequency furnace outlet cooling tank 10.
As shown in fig. 1 and 3, the second circulation system further includes a coating bath 7 disposed at the front end of the hot water washing bath 8 and a first small cooling bath 11 disposed at the rear end of the outlet water cooling bath 10 of the intermediate frequency furnace, the coating bath 7 is connected with a second heat exchanger 15, the inlet end of the second heat exchanger 15 is connected with the outlet end of the water cooling bath pipeline pump 18, and the outlet end of the second heat exchanger 15 is connected with the first small cooling bath 11. A third heat exchanger 17 is connected between the outlet end of the second heat exchanger 15 and the first small cooling tank 11, the second heat exchanger 15 is a plating tank plate heat exchanger, and the third heat exchanger 17 is a cooling plate heat exchanger.
As shown in fig. 1 and 3, the second circulation system further includes a soap dipping tank 14 disposed at the rear end of the water cooling tank 10 at the outlet of the intermediate frequency furnace, a fourth heat exchanger 19 is disposed in the soap dipping tank 14, the inlet end of the fourth heat exchanger 19 is connected to the outlet end of the water cooling tank pipeline pump 18, the outlet end of the fourth heat exchanger 19 is connected to the first small cooling tank 11, and the fourth heat exchanger 19 is a stainless steel heat exchanger. A second small cooling tank 12 and a phosphorization tank 13 are also sequentially arranged between the first small cooling tank 11 and the soap dipping tank 14.
When the plating line is produced, the steel wire is heated by the open fire furnace, and then cooled in the water cooling tank 1 at the outlet of the open fire furnace, and then the steel wire surface is treated by the first acid tank 3, the second acid tank 4 and the third acid tank 5 in sequence, and then enters the plating tank 7 to perform surface zinc plating and copper plating, and then enters the hot water washing tank 8 to clean the surface, and then enters the intermediate frequency furnace 9 to realize thermal diffusion, and then enters the water cooling tank 10 at the outlet of the intermediate frequency furnace, the first small cooling tank 11 and the second small cooling tank 12 to perform tertiary cooling, and after the tertiary cooling, the steel wire is phosphorized in the phosphorization tank 13, and then enters the soap soaking tank 14 and finally the plating take-up machine.
The embodiment provides an electroplating heat energy recycling method, and the electroplating heat energy recycling system comprises the following steps:
cooling the steel wire subjected to heat treatment by the open fire furnace in a water cooling tank 1 at the outlet of the open fire furnace, heating the cooling water to be hot water at the temperature of 90 +/-5 ℃, pumping out the hot water by a filter circulating pump 2, filtering the hot water, feeding the filtered hot water into each first heat exchanger 6 of a first acid tank 3, a second acid tank 4 and a third acid tank 5, heating the acid liquid in the acid tanks to the temperature of 65 +/-5 ℃, and making cold water generated after heat exchange flow back to the water cooling tank 1 at the outlet of the open fire furnace;
the steel wire treated by the intermediate frequency furnace 9 is cooled in a water cooling tank 1 at the outlet of the intermediate frequency furnace, cooling water is heated to be hot water at 90 +/-5 ℃, a pipeline pump 18 of the water cooling tank pumps out the hot water, the hot water is distributed to a second heat exchanger 15 connected with a plating tank 7, a hot water washing tank 8 and a fourth heat exchanger 19 in a soap dipping tank 14 to be heated, plating solution in the plating tank 7 enters the second heat exchanger 15 to be heated to 49 +/-5 ℃, the water temperature in the hot water washing tank 8 is heated to 86 +/-5 ℃, and the temperature of a lubricant in the soap dipping tank 14 is heated to 77 +/-5 ℃ through the fourth heat exchanger 19 to meet the use requirement; after the steel wire is cleaned in the hot water washing tank 8, the water in the hot water washing tank 8 is cooled and flows back to the water cooling tank 1 at the outlet of the intermediate frequency furnace, and the cold water generated by the second heat exchanger 15 and the fourth heat exchanger 19 flows into the first small cooling tank 11 at the rear end of the water cooling tank 10 at the outlet of the intermediate frequency furnace.
In the second circulating system, the plating tank 7 and the soap dipping tank 14 are heated by using heat exchangers, liquid in the two tanks is not mixed with hot water in the water cooling tank 10 at the outlet of the intermediate frequency furnace, and only return water in the hot water washing tank 8 uses the hot water washing tank pipeline pump 16, so that the liquid level balance and the temperature in each tank can be kept by controlling the water flow rate into and out of the hot water washing tank 8. In addition, the temperature of the cooling water in the first small cooling tank 11 can be controlled by controlling the flow of the cooling water in the third heat exchanger 17, the temperature of the cooling water in the second small cooling tank 12 is controlled by controlling the flow of the supplemented water through temperature control, and the temperature of the phosphoric acid in the phosphating tank 13 can be controlled by cooling the steel wire for three times, so that the technological requirements are met.
According to the invention, the hot water generated by the water cooling tank at the outlet of the open fire furnace is used for heating the acid liquid in each acid tank, and the cold water generated after heat exchange flows back to the outlet of the open fire furnace for cooling, so that heat circulation is realized, additional steam or cooling equipment is not required, the production cost is reduced, and the liquid level balance of each tank body is kept.
The above description is only a preferred embodiment of the present invention, and it should be noted that, for those skilled in the art, several modifications and variations can be made without departing from the technical principle of the present invention, and these modifications and variations should also be regarded as the protection scope of the present invention.
Claims (10)
1. An electroplating heat energy recycling system is characterized by comprising a first circulating system and a second circulating system which are sequentially arranged;
the first circulating system comprises a naked furnace outlet water cooling tank and a plurality of acid tanks which are sequentially arranged, a first heat exchanger is arranged in each acid tank, and hot water in the naked furnace outlet water cooling tank and cold water in the first heat exchanger circulate;
the second circulating system comprises a hot water washing tank and an intermediate frequency furnace outlet water cooling tank which are sequentially arranged, and hot water in the intermediate frequency furnace outlet water cooling tank and cold water in the hot water washing tank circulate.
2. The electroplating heat energy recycling system of claim 1, wherein the open fire furnace outlet water cooling tank is connected with the inlet end of the first heat exchanger through a filter circulating pump, and the outlet end of the first heat exchanger is connected with the open fire furnace outlet water cooling tank.
3. The electroplating heat energy recycling system of claim 2, wherein the number of the acid tanks is three, and the system comprises a first acid tank, a second acid tank and a third acid tank which are arranged in sequence, two first heat exchangers are arranged in each acid tank, and the first heat exchangers are PP heat exchangers.
4. The electroplating heat energy recycling system according to claim 1, wherein the intermediate frequency furnace outlet cooling tank is connected with an inlet end of a water cooling tank pipeline pump, an outlet end of the water cooling tank pipeline pump is connected with the hot water washing tank, the hot water washing tank is connected with an inlet end of a hot water washing tank pipeline pump, and an outlet end of the hot water washing tank pipeline pump is connected with the intermediate frequency furnace outlet cooling tank.
5. The electroplating heat energy recycling system according to claim 4, wherein the second circulating system further comprises a coating bath arranged at the front end of the hot water washing bath and a first small cooling bath arranged at the rear end of the water cooling bath at the outlet of the intermediate frequency furnace, the coating bath is connected with a second heat exchanger, the inlet end of the second heat exchanger is connected with the outlet end of the water cooling bath pipeline pump, and the outlet end of the second heat exchanger is connected with the first small cooling bath.
6. The electroplating heat energy recycling system of claim 5, wherein a third heat exchanger is further connected between the outlet end of the second heat exchanger and the first small cooling tank, the second heat exchanger is a plating tank plate heat exchanger, and the third heat exchanger is a cooling plate heat exchanger.
7. The electroplating heat energy recycling system of claim 4, wherein the second circulating system further comprises a soaping tank arranged at the rear end of a water cooling tank at the outlet of the intermediate frequency furnace, a fourth heat exchanger is arranged in the soaping tank, the inlet end of the fourth heat exchanger is connected with the outlet end of a water cooling tank pipeline pump, the outlet end of the fourth heat exchanger is connected with the first small cooling tank, and the fourth heat exchanger is a stainless steel heat exchanger.
8. The electroplating heat energy recycling system of claim 7, wherein a second small cooling tank and a phosphating tank are sequentially arranged between the first small cooling tank and the soap dipping tank.
9. A plating heat energy recycling method, which is characterized in that the plating heat energy recycling system of any one of claims 1 to 8 is adopted, and the method comprises the following steps:
cooling the steel wire treated by the open fire furnace in a water cooling tank at the outlet of the open fire furnace, heating the cooling water to be hot water at the temperature of 90 +/-5 ℃, filtering the hot water, then feeding the hot water into a first heat exchanger of an acid tank, heating acid liquid in the acid tank to the temperature of 65 +/-5 ℃, and returning cold water generated after heat exchange to the water cooling tank at the outlet of the open fire furnace;
the steel wire after the intermediate frequency furnace is handled cools down in intermediate frequency furnace export water cooling tank, heats the cooling water for 90 +/-5 ℃ hot water, and the hot water flows into hot water wash bowl, makes the temperature in the hot water wash bowl heat to 86 +/-5 ℃, and the steel wire makes the water cooling in the hot water wash bowl after the surface is washd in hot water wash bowl to flow back to intermediate frequency furnace export water cooling tank.
10. The electroplating heat energy recycling method according to claim 9, characterized in that the hot water in the water cooling tank at the outlet of the intermediate frequency furnace is further branched to a second heat exchanger connected with the plating tank and a fourth heat exchanger in the soap dipping tank for heating, the plating solution in the plating tank enters the second heat exchanger to be heated to 49 +/-5 ℃, the lubricant temperature in the soap dipping tank is heated to 77 +/-5 ℃ through the fourth heat exchanger, and the cold water generated by the second heat exchanger and the fourth heat exchanger flows to a first small cooling tank at the rear end of the water cooling tank at the outlet of the intermediate frequency furnace.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202110282032.5A CN113106514B (en) | 2021-03-16 | 2021-03-16 | Electroplating heat energy recycling system and method |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202110282032.5A CN113106514B (en) | 2021-03-16 | 2021-03-16 | Electroplating heat energy recycling system and method |
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| CN113106514A true CN113106514A (en) | 2021-07-13 |
| CN113106514B CN113106514B (en) | 2023-03-03 |
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Citations (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN201442987U (en) * | 2009-07-27 | 2010-04-28 | 山东胜通集团股份有限公司 | Steel-cord plating and waste-water utilizing automatic-control system |
| CN202124667U (en) * | 2011-06-20 | 2012-01-25 | 江阴三知工控机械有限公司 | Brass electroplating production line |
| CN202485491U (en) * | 2012-03-30 | 2012-10-10 | 无锡市盛力达机械工程有限公司 | Waste heat recycling device of water cooling tank |
| CN204620659U (en) * | 2015-02-13 | 2015-09-09 | 张家港市骏马钢帘线有限公司 | Cooling recirculation system |
| CN204958972U (en) * | 2015-08-21 | 2016-01-13 | 张伟飞 | Steel production waste heat recovery cooling device |
| CN206956161U (en) * | 2017-06-21 | 2018-02-02 | 惠州市南钢金属压延有限公司 | Waste heat recycle device |
| CN110538889A (en) * | 2019-09-10 | 2019-12-06 | 江苏兴达钢帘线股份有限公司 | Method for interchanging rubber pipeline and heat treatment line |
| CN110965111A (en) * | 2019-12-24 | 2020-04-07 | 天津敏信机械有限公司 | Improved device for electroplating cooling circulation line |
| CN210374706U (en) * | 2019-07-10 | 2020-04-21 | 河南恒星科技股份有限公司 | Heat exchange coil for rinsing bath |
| CN210367924U (en) * | 2019-07-11 | 2020-04-21 | 河南恒星科技股份有限公司 | Steel cord rinsing bath internal circulation system |
| CN210374714U (en) * | 2019-07-11 | 2020-04-21 | 河南恒星科技股份有限公司 | Waste heat utilization system for waste hot water of cooling tank |
-
2021
- 2021-03-16 CN CN202110282032.5A patent/CN113106514B/en active Active
Patent Citations (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN201442987U (en) * | 2009-07-27 | 2010-04-28 | 山东胜通集团股份有限公司 | Steel-cord plating and waste-water utilizing automatic-control system |
| CN202124667U (en) * | 2011-06-20 | 2012-01-25 | 江阴三知工控机械有限公司 | Brass electroplating production line |
| CN202485491U (en) * | 2012-03-30 | 2012-10-10 | 无锡市盛力达机械工程有限公司 | Waste heat recycling device of water cooling tank |
| CN204620659U (en) * | 2015-02-13 | 2015-09-09 | 张家港市骏马钢帘线有限公司 | Cooling recirculation system |
| CN204958972U (en) * | 2015-08-21 | 2016-01-13 | 张伟飞 | Steel production waste heat recovery cooling device |
| CN206956161U (en) * | 2017-06-21 | 2018-02-02 | 惠州市南钢金属压延有限公司 | Waste heat recycle device |
| CN210374706U (en) * | 2019-07-10 | 2020-04-21 | 河南恒星科技股份有限公司 | Heat exchange coil for rinsing bath |
| CN210367924U (en) * | 2019-07-11 | 2020-04-21 | 河南恒星科技股份有限公司 | Steel cord rinsing bath internal circulation system |
| CN210374714U (en) * | 2019-07-11 | 2020-04-21 | 河南恒星科技股份有限公司 | Waste heat utilization system for waste hot water of cooling tank |
| CN110538889A (en) * | 2019-09-10 | 2019-12-06 | 江苏兴达钢帘线股份有限公司 | Method for interchanging rubber pipeline and heat treatment line |
| CN110965111A (en) * | 2019-12-24 | 2020-04-07 | 天津敏信机械有限公司 | Improved device for electroplating cooling circulation line |
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| Publication number | Publication date |
|---|---|
| CN113106514B (en) | 2023-03-03 |
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